Process control for long chain branching control in polyethylene production

Patent metadata

Field	Value
Publication number	US-10155831-B2
Application number	US-201615277726-A
Country	US
Kind code	B2
Filing date	Sep 27, 2016
Priority date	Sep 5, 2013
Publication date	Dec 18, 2018
Grant date	Dec 18, 2018

Abstract

Polymerization process control methods for making polyethylene are provided. The process control methods include performing a polymerization reaction in a polymerization reactor to produce the polyethylene, where ethylene, and optionally one or more comonomers, in the polymerization reaction is catalyzed by an electron donor-free Ziegler-Natta catalyst and an alkyl aluminum co-catalyst. A melt flow ratio (I 21 /I 2 ) of the polyethylene removed from the polymerization reactor is measured and an amount of long chain branching (LCB) of the polyethylene from the polymerization reactor is controlled by adjusting a weight concentration of the alkyl aluminum co-catalyst present in the polymerization reactor. In addition, an electron donor-free Ziegler-Natta catalyst productivity of the polyethylene being produced in the polymerization reactor is measured from which the amount of LCB of the polyethylene from the polymerization reactor is determined using the measured electron donor-free Ziegler-Natta catalyst productivity and a predetermined relationship between the electron donor-free Ziegler-Natta catalyst productivity and the LCB.

First claim

What is claimed is:

1. A polymerization process control method, comprising:
performing a polymerization reaction in a polymerization reactor to produce polyethylene, wherein the polymerization reaction is catalyzed by an electron donor-free Ziegler-Natta catalyst and an alkyl aluminum co-catalyst with ethylene and optionally one or more comonomers to produce the polyethylene;
removing a portion of the polyethylene from the polymerization reactor;
measuring a melt flow ratio (I 21 /I 2 ) of the polyethylene removed from the polymerization reactor to determine the amount of long chain branching (LCB) using a predetermined relationship between the melt flow ratio (I 21 /I 2 ) and the LCB; and
controlling an amount of long chain branching (LCB) of the polyethylene from the polymerization reactor by adjusting a weight concentration of the alkyl aluminum co-catalyst present in the polymerization reactor.

2. The polymerization process control method of claim 1 , wherein adjusting the weight concentration of the alkyl aluminum co-catalyst present in the polymerization reactor is done by changing a mole ratio of the alkyl aluminum co-catalyst to active metal in the electron donor-free Ziegler-Natta catalyst.

3. The polymerization process control method of claim 1 , further including varying a weight concentration of the alkyl aluminum co-catalyst in the polymerization reactor while performing the polymerization reaction, thereby changing the melt flow ratio (I 21 /I 2 ) of the polyethylene from the polymerization reactor to make a predetermined change in at least the LCB or to bring the LCB in the polyethylene into compliance with a predetermined product specification set.

4. The polymerization process control method of claim 3 , including:
generating melt flow ratio (I 21 /I 2 ) data and LCB data from polyethylene produced while varying the weight concentration of the alkyl aluminum co-catalyst in the polymerization reactor; and
developing the predetermined relationship between the melt flow ratio (I 21 /I 2 ) and the LCB from the melt flow ratio (I 21 /I 2 ) data and LCB data.

5. The polymerization process control method of claim 1 , wherein controlling the amount of LCB includes decreasing the weight concentration of the alkyl aluminum co-catalyst present in the polymerization reactor to increase the LCB of the polyethylene produced in the polymerization reactor.

6. The polymerization process control method of claim 1 , wherein the polyethylene has LCB greater than about 0.01 per 1,000 carbon atoms and less than about 0.07 per 1,000 carbon atoms; and wherein the polyethylene has a melt flow ratio (I 21 /I 2 ) ranging from about 35 to about 55 or a density of from 0.91 g/cm 3 to about 0.965 g/cm 3 .

7. The polymerization process control method of claim 1 , wherein the electron donor-free Ziegler-Natta catalyst is formed by a process that comprises:
combining one or more supports with one or more magnesium-containing compounds under reaction conditions to form a first reacted product;
combining one or more chloro substituted silanes with the first reacted product under reaction conditions to form a second reacted product; and
combining one or more titanium halides with the second reacted product under reaction conditions to form the electron donor-free Ziegler-Natta catalyst,
wherein the one or more supports comprises silica, alumina, or a combination thereof
wherein the one or more magnesium-containing compounds has the formula: R 1 —Mg—R 2 , wherein R 1 and R 2 are independently selected from the group consisting of hydrocarbyl groups and halogen atoms.

8. The polymerization process control method of claim 1 , wherein the alkyl aluminum co-catalyst is triethylaluminum (TEAl), triisobutylaluminum, tri-n-butylaluminum, tri-n-hexylaluminum, tri-n-octylaluminum, trimethylaluminum or any combination thereof.

9. The polymerization process control method of claim 1 , wherein the polymerization reactor is selected from the group consisting of a solution reactor, a slurry loop reactor, a supercritical loop reactor, a stirred-bed gas-phase reactor, or a fluidized-bed, gas-phase reactor.

10. A polymerization method, comprising:
performing a polymerization reaction in a polymerization reactor to produce polyethylene, wherein the polymerization reaction is catalyzed by an electron donor-free Ziegler-Natta catalyst and an alkyl aluminum co-catalyst with ethylene and optionally one or more comonomers to produce the polyethylene;
removing a portion of the polyethylene from the polymerization reactor;
measuring a melt flow ratio (I 21 /I 2 ) of the polyethylene removed from the polymerization reactor; and
determining an amount of long chain branching (LCB) of the polyethylene from the polymerization reactor using the measured melt flow ratio and a predetermined relationship between the melt flow ratio (I 21 /I 2 ) and the LCB.

Assignees

• Univation Tech Llc

Inventors

• Mariott Wesley R
• Cann Kevin J
• Moorhouse John H
• Goode Mark G
• Oswald Thomas

Classifications

• C08F2500/09

  Long chain branches · CPC title

• C08F110/02

  Ethene · CPC title

• C08F2400/02

  Control or adjustment of polymerization parameters · CPC title

• C08F210/16 Primary

  Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title

• C08F4/76

  selected from titanium, zirconium, hafnium, vanadium, niobium or tantalum · CPC title